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Applied and Environmental Microbiology, November 1998, p. 4340-4345, Vol. 64, No. 11
Nishiki Research Laboratories,
Received 29 December 1997/Accepted 4 September 1998
A trehalose synthase (TSase) that catalyzes the synthesis of
trehalose from D-glucose and Trehalose
(1- Our approach to trehalose production is to use an enzymatic process to
produce trehalose from sucrose, one of the least expensive sugars.
Since sucrose is efficiently converted to Our objectives were (i) to screen microorganisms, primarily fungi, for
TSase activity; (ii) to purify and characterize the TSase; (iii) to
identify the enzymatic process by which trehalose is produced from
sucrose; and (iv) to identify an enzymatic process for production of
trehalose from sucrose in which the fructose component is also
converted to trehalose.
Materials.
Microorganisms and culture conditions.
Microorganisms were
obtained mainly from the Institute of Fermentation, Osaka, Japan
(IFO), and the Institute of Applied Microbiology. Some of the
microorganisms tested were obtained from a culture collection in the
Nishiki Research Laboratory. Basidiomycetes were grown at 26°C for 7 to 10 days in GYM medium (pH 5.5), which contained the following, in
grams per liter: yeast extract (Difco, Detroit, Mich.), 7.5; malt
extract (Difco), 2; KH2PO4, 5;
MgSO4 · 7H2O, 0.5; and glucose or
trehalose, 40. Other fungi were grown at 28°C for 3 to 5 days in GYMB
medium (pH 6.2), which contained the following, in grams per liter:
yeast extract, 6; malt extract, 6; Bacto Peptone (Difco), 10; glucose,
10; and trehalose, 20. Yeasts were grown in YPT medium (pH 6.0), which
contained the following, in grams per liter: trehalose, 20; yeast
extract, 10; and Bacto Peptone, 20.
Enzyme assay.
The mycelia of fungi and basidiomycetes were
collected, disrupted with an HG-30 homogenizer (Hitachi Co., Ltd.,
Tokyo, Japan) and centrifuged to give a supernatant for the trehalose
phosphorolysis assay. For the trehalose synthesis assay, the crude
sample was applied to a 20-ml DEAE-Toyopearl 650C column (Tosoh Co.
Ltd., Tokyo, Japan) equilibrated with 20 mM potassium phosphate buffer (pH 7.0) and proteins were eluted with a linear gradient of 20 to 500 mM KCl in a total volume of 200 ml. Fractions showing trehalose phosphorolysis activity were collected and concentrated with a hollow
fiber ultrafiltration apparatus (Minimodule nM-3; Asahi Kasei Co. Ltd.,
Tokyo, Japan) to give a concentrated crude enzyme sample. For
preparation of crude enzyme samples from yeasts, a similar procedure
was used except that cells were disrupted with a high-speed
shaking-disrupting apparatus (Michael Co. Ltd.).
0099-2240/98/$04.00+0
Copyright © 1998, American Society for Microbiology. All rights reserved.
Purification and Characterization of a Trehalose
Synthase from the Basidiomycete Grifola
frondosa
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ABSTRACT
Top
Abstract
Introduction
Materials & Methods
Results
Discussion
References
-D-glucose
1-phosphate (
-D-glucose 1-P) was detected in a
basidiomycete, Grifola frondosa. TSase was purified
106-fold to homogeneity with 36% recovery by ammonium sulfate
precipitation and several steps of column chromatography. The native
enzyme appears to be a dimer since it has apparent molecular masses of
120 kDa, as determined by gel filtration column chromatography, and 60 kDa, as determined by sodium dodecyl sulfate-polyacrylamide gel
electrophoresis. Although TSase catalyzed the phosphorolysis of
trehalose to D-glucose and
-D-glucose 1-P,
in addition to the synthesis of trehalose from the two substrates, the
TSase equilibrium strongly favors trehalose synthesis. The optimum
temperatures for phosphorolysis and synthesis of trehalose were 32.5 to
35°C and 35 to 37.5°C, respectively. The optimum pHs for these
reactions were 6.5 and 6.5 to 6.8, respectively. The substrate
specificity of TSase was very strict: among eight disaccharides
examined, only trehalose was phosphorolyzed, and only
-D-glucose 1-P served as a donor substrate with
D-glucose as the acceptor in trehalose synthesis. Two
efficient enzymatic systems for the synthesis of trehalose from sucrose
were identified. In system I, the
-D-glucose 1-P
liberated by 1.05 U of sucrose phosphorylase was linked with D-glucose by 1.05 U of TSase, generating trehalose at the
initial synthesis rate of 18 mmol/h in a final yield of 90 mol% under optimum conditions (300 mM each sucrose and glucose, 20 mM inorganic phosphate, 37.5°C, and pH 6.5). In system II, we added 1.05 U of
glucose isomerase and 20 mM MgSO4 to the reaction mixture
of system I to convert fructose, a by-product of the sucrose
phosphorylase reaction, into glucose. This system generated trehalose
at the synthesis rate of 4.5 mmol/h in the same final yield.
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INTRODUCTION
Top
Abstract
Introduction
Materials & Methods
Results
Discussion
References
-D-glucopyranosyl-
-D-glucopyranoside)
is a nonreducing disaccharide with an
,
-1,1 glycosidic linkage
and is widely distributed in plants, insects, fungi, yeast, and
bacteria (7). Due to the absence of reducing ends in
trehalose, it is highly resistant to heat, pH, and Maillard's reaction
(24). In trehalose-producing organisms, this compound may
serve as an energy reserve, a buffer against stresses such as
desiccation and freezing, and a protein stabilizer (5, 7, 26, 31, 32). If trehalose can be produced economically, then it has potential commercial applications as a sweetener, a food stabilizer, and an additive in cosmetics and pharmaceuticals (6, 25). Recently, trehalose production through fermentation of yeast
(17) and Corynebacterium (30),
enzymatic processes from starch (18, 34) and maltose
(19, 22, 23, 33), and extraction from transformed plants
(10) has been reported.
-D-glucose 1-phosphate (
-D-glucose 1-P) and fructose by sucrose
phosphorylase (SPase), we screened microorganisms for an enzyme that
converts
-D-glucose 1-P to trehalose on the assumption
that the combination of the putative trehalose synthase (TSase) and
SPase would convert sucrose into trehalose. Although similar enzyme
activities have been reported in the basidiomycete Flammulina
velutipes (11) and in the yeast Pichia
fermentans (27), these enzymes have not been well characterized.
![]()
MATERIALS AND METHODS
Top
Abstract
Introduction
Materials & Methods
Results
Discussion
References
-D-Glucose 1,6-bisphosphate
(glucose 1,6-P), phosphoglucomutase (PGM; from rabbit muscle) (EC
5.4.2.2), and glucose-6-phosphate 1-dehydrogenase (G6PDH; from yeast)
(EC 1.1.1.49) were purchased from Boehringer Mannheim Co., Ltd. (Tokyo,
Japan). SPase (from Leuconostoc mesenteroides) (EC 2.4.1.7)
was purchased from Kikkoman Co. Ltd. (Tokyo, Japan). Glucose isomerase
(GIase; from Streptomyces phaeochromogenes) (EC 5.3.1.18)
was purified from a commercially available immobilized enzyme solution
(Nagase Biochemical, Osaka, Japan) by DEAE column chromatography and
gel filtration chromatography on a high-performance liquid
chromatograph to remove glucose 1-P-degrading activity and
glucose oxidase-like activity.
-NADP+, trehalose,
and other sugars were obtained from Wako Pure Chemicals (Tokyo, Japan).
D-glucose +
-D-glucose 1-P). The amount of the
-D-glucose 1-P produced was determined by coupling the
TSase activity with PGM (
-D-glucose
1-P
-D-glucose 6-P) and G6PDH
(
-D-glucose 6-P + NADP+
6-phospho-D-gluconolactone + NADPH + H+). NADPH generation was measured by the
change in absorbance at 340 nm and was assumed to be proportional to
TSase activity. The reaction mixture contained 200 mM trehalose, 40 mM
potassium phosphate buffer (pH 7.0), 10 mM glutathione, 16 µM EDTA, 1 mM NADP+, 1.3 mM MgCl2 · 6H2O, 67 µM glucose 1,6-P, 1.55 U of PGM per ml, 1.75 U
of G6PDH per ml, and an enzyme sample, in a total volume of 2 ml.
During incubation at 30°C, the change in absorbance at 340 nm was
monitored with an automated spectrophotometer (Shimadzu model UV-2200).
One unit of enzyme activity was defined as the amount of enzyme that
catalyzed the formation of 1 µmol of
-glucose 1-P per min, and
specific activity was expressed as the number of units of enzyme
per milligram of protein. Protein concentrations were measured
with a protein assay kit (Bio-Rad Laboratories, Tokyo, Japan) using
bovine serum albumin as the standard.
-glucose 1-P. The reaction mixture contained 100 mM
-glucose 1-P,
100 mM
-D-glucose 1-P, 100 mM HEPES buffer (pH 7.0), and an enzyme sample, in a total volume of 250 µl. Reaction mixtures were
incubated at 35°C for 3 h and stopped by boiling for 5 min. The
trehalose produced was measured by high-performance liquid chromatography (HPLC) on a Shimadzu LC-10A system equipped with a
YMC-pack polyamine II column (4.6 by 250 mm) and a refraction index
detector (Shimadzu RID-6A). The solvent system was 70%
acetonitrile-30% H2O with a flow rate of 1.0 ml/min.
Gel electrophoresis.
Sodium dodecyl sulfate
(SDS)-polyacrylamide gel electrophoresis (13) was done with
the Pharmacia Phast system. After electrophoresis, proteins were
stained with the Phast gel protein silver stain kit. For measurement of
the molecular mass of TSase, the following standard proteins were used;
phosphorylase b (94 kDa), bovine serum albumin (67 kDa),
ovalbumin (43 kDa), carbonic anhydrase B (30 kDa), soybean trypsin
inhibitor (20.1 kDa), and
-lactalbumin (14.4 kDa).
Purification of TSase from G. frondosa. TSase was monitored by assaying trehalose phosphorolysis activity. All the operations were done in a cold room (4°C) unless otherwise specified.
(i) Step 1. Preparation of cell extract. Fruiting bodies of G. frondosa (wet weight, 611 g) were suspended in 1.2 liters of cold 20 mM potassium phosphate buffer (pH 7.0) containing 20% (vol/vol) glycerol, 1 mM EDTA, and 1 mM dithiothreitol and disrupted with a Waring blender. Cell debris was removed by centrifugation at 12,000 × g for 20 min, and the supernatant was used as the cell extract.
(ii) Step 2. Ammonium sulfate fractionation. Solid ammonium sulfate was added to the cell extract to give a concentration of 40% (wt/vol), and the mixture was left standing overnight. The next morning, the mixture was centrifuged to remove insoluble material, yielding 1,560 ml of the enzyme solution.
(iii) Step 3. Butyl-Toyopearl column chromatography. We applied the enzyme solution to a butyl-Toyopearl 650C column (2.4 by 24 cm; Tosoh) equilibrated with 20 mM potassium phosphate buffer (pH 7.0) containing 40% ammonium sulfate. The adsorbed enzyme was eluted with a linear gradient of 40 to 0% ammonium sulfate in the same buffer in a total volume of 800 ml. The enzyme activity was eluted at approximately 10% ammonium sulfate. The active fractions (250 ml) were pooled and dialyzed against two changes of 5 liters of 20 mM potassium phosphate buffer (pH 7.0).
(iv) Step 4. SuperQ-Toyopearl column chromatography. The dialyzed solution was applied to a SuperQ-Toyopearl 650M column (2.5 by 17 cm; Tosoh) equilibrated with 20 mM potassium phosphate buffer (pH 7.0). The column was washed and proteins were eluted with a linear gradient of 0 to 0.2 M KCl in the same buffer in a total volume of 600 ml. Active fractions (160 ml) that were eluted at approximately 0.1 M KCl were combined and dialyzed against 5 liters of 20 mM potassium phosphate buffer (pH 6.0). The pH was adjusted for the next column chromatography step.
(v) Step 5. AF-Blue-Toyopearl column chromatography. The dialyzed solution was applied to an Affinity (AF)-Blue-Toyopearl 650ML column (1.0 by 17 cm; Tosoh) equilibrated with 20 mM potassium phosphate buffer (pH 6.0). After the column had been washed, proteins were eluted with a linear gradient of 0 to 2 M KCl in the same buffer in a total volume of 400 ml. TSase activity was eluted at approximately 0.8 M KCl. The active fractions (220 ml) were combined and dialyzed against 5 liters of 20 mM potassium phosphate buffer (pH 6.0).
(vi) Step 6. AF-Red-Toyopearl column chromatography. An AF-Red-Toyopearl 650ML column (1.0 by 17 cm; Tosoh) was equilibrated with 20 mM potassium phosphate buffer (pH 7.0). TSase was eluted with a linear gradient (0 to 2 M) of KCl in the same buffer in a total volume of 400 ml. TSase activity (210 ml) that was eluted at 0.8 M KCl was pooled and dialyzed against 5 liters of 20 mM potassium phosphate buffer (pH 7.0).
(vii) Step 7. Rechromatography on a SuperQ-Toyopearl column. TSase was further purified by rechromatography on a SuperQ-Toyopearl 650M column (0.7 by 4.5 cm). The buffer was the same as that used in step 4. TSase was eluted with a linear gradient of 0 to 100 mM KCl in a total volume of 400 ml. The active fractions (170 ml) that were eluted at approximately 30 mM KCl were combined and dialyzed against the same buffer. In step 4, the enzyme was eluted at 100 mM KCl in a steeper linear gradient, which was probably higher than the true concentration.
(viii) Step 8. TSK gel G3000SW column chromatography. The dialyzed solution was applied to a TSK gel G3000SW column (0.75 by 30 cm) equilibrated with 20 mM potassium phosphate buffer (pH 7.0) in an HPLC system. Proteins were eluted with the same buffer at a constant flow rate of 0.5 ml/min. TSase was detected at 16 min, giving a single sharp peak.
Characterization of TPase. For determination of optimal pH, pH stability, heat stability, and substrate specificity of TSase, the above-described reaction and assay conditions for trehalose phosphorolysis and synthesis were used, except where otherwise specified. The following buffer systems were used: acetate-Na buffer (pH 4.0-5.5), morpholineethanesulfonic acid (MES) (pH 5.5 to 7.0), HEPES (pH 7.0 to 8.0), Tris-HCl (pH 7.5 to 9.0), and glycine-NaOH (pH 8.5 to 12.0).
CES I.
SPase liberates
-D-glucose 1-P and
fructose from sucrose. In coupled enzyme system I (CES I), the
-D-glucose 1-P liberated from sucrose by the action of
SPase was linked with glucose to produce trehalose by the trehalose
synthesis activity of TSase. The standard reaction mixture contained
300 mM sucrose, 300 mM glucose, 10 mM Pi, 1.05 U of SPase
per ml, and 1.05 U of TSase per ml in 100 mM MES buffer (pH 6.5). For
maximal production of trehalose, the mixture was incubated at various
temperatures and pHs.
CES II.
Coupled enzyme system II (CES II) was designed to
convert the fructose liberated from sucrose by SPase in CES I to
glucose by the action of GIase, which was then linked with
-D-glucose 1-P to yield trehalose. The reaction mixture
for CES II consisted of 300 mM sucrose, 20 mM Pi, 20 mM
MgSO4, and 1.05 U of TSase, SPase, and GIase each per ml in
100 mM HEPES (pH 7.0). The amounts of trehalose, sucrose, glucose, and
fructose were determined by HPLC, and the amount of
-D-glucose 1-P was determined by the enzyme assay
described above.
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RESULTS |
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Screening of microorganisms.
We collected ascomycetes,
basidiomycetes, zygomycetes, and imperfect (mitosporic)
fungi from various culture collections to determine if they
produced TSase. Among 132 strains tested, most strains had at least
some trehalose phosphorolysis activity. We then examined trehalose
phosphorolysis-positive strains to determine if they also could
synthesize trehalose from
-D-glucose 1-P and D-glucose (Table 1). Among
these strains, G. frondosa CM 236 had the highest activity,
although the phosphorolysis activity of this strain was not very high.
This strain had the same activity in both glucose- and
trehalose-containing media, suggesting that TSase was produced
constitutively.
|
Purification of TSase from G. frondosa. We purified TSase 106-fold with 36% recovery (Table 2). The purified TSase gave a single protein band with an apparent molecular mass of 60 kDa on SDS-polyacrylamide gel electrophoresis (Fig. 1). The specific activity of the purified enzyme was 4.2 U.
|
|
-D-glucose 1-P (23% conversion; equilibrium constant,
i.e., [
-D-glucose 1-P][glucose]/[trehalose][Pi], 0.085) (Fig.
2). When a reaction mixture containing
0.2 U of TSase per ml and a 25 mM concentration each of
-D-glucose 1-P and glucose was incubated at 35°C and pH 7.0 for 48 h, 16 mM trehalose (65% conversion; equilibrium constant, i.e.,
[trehalose][Pi]/[
-D-glucose
1-P][glucose], 3.5) was produced (Fig. 2). We concluded that the
equilibrium of TSase under these reaction conditions was toward the
synthesis of trehalose.
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Characterization of TSase. The following enzymatic properties of TSase were determined with the purified enzyme: (i) molecular mass; (ii) optimum temperature and heat stability; (iii) optimum pH and pH stability; (iv) effects of cations on TSase activity; and (v) substrate specificity.
(i) Molecular mass. The relative molecular mass of TSase was 60 kDa by SDS-polyacrylamide gel electrophoresis and that of the native enzyme was 120 kDa by HPLC gel filtration (Fig. 1), suggesting that TSase is composed of two identical 60-kDa subunits. We did not study dilution dissociation of TSase any further.
(ii) Optimum temperature and heat stability. Trehalose phosphorylation and synthesis activities measured as a function of temperature from 0 to 50°C showed that the former and latter activities were highest at 32.5 and 37.5°C, respectively (Fig. 3A). When these reaction mixtures were preincubated for 30 min at various temperatures, the trehalose phosphorolysis activity was stable up to 35°C but decreased rapidly at temperatures above that (Fig. 3B). The trehalose synthesis activity was stable up to 32.5°C (Fig. 3B).
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(iii) Optimum pH and pH stability. The trehalose phosphorylation and synthesis activities of TSase were measured at various pHs in buffers that had the same ionic concentrations. The phosphorolysis and synthesis activities were the highest at pH 6.5 and pH 6.5 to 6.8, respectively (Fig. 4A). After a 24-h incubation of the enzyme solution in buffer, the phosphorylation activity was highest at pH 8.3 (Fig. 4B), and the synthesis activity was highest between pH 5.5 and 9.0 (Fig. 4B).
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(iv) Effects of cations on TSase activity. The presence of EDTA did not affect trehalose phosphorylation or synthesis activities, which showed that TSase required no cations for the activity. Cu2+ at 1 mM completely abolished both phosphorylation and synthesis activities. At 0.1 mM Cu2+, phosphorylation and synthesis activities were reduced to 76 and 48%, respectively. Zn2+ at 1 mM also reduced the phosphorolysis and synthesis activities to 40 and 0%, respectively. Other cations, Mn2+, Fe3+, Co2+, Ca2+, Mg2+, Ba2+, K+, Na+, Al3+, Rb+, and Cs+, showed no significant effect on TSase.
(v) Substrate specificity.
TSase phosphorylation was specific
for trehalose, and no activity was detected with other disaccharides,
such as neotrehalose, palatinose, cellobiose, lactose, sucrose,
maltose, or isomaltose. TSase synthesis activity was also very
specific. When
-D-glucose 1-P was used as a
substrate donor, only D-glucose served as the acceptor. L-Glucose, D-galactose,
D-mannose, D-xylose, D-fructose, D-sorbitol, D-mannitol, or
D-fucose did not serve as the acceptor. When
-glucose
1-P,
-D-galactose 1-P,
-D-mannose 1-P, or
-D-xylose 1-P was used as a substrate donor and
D-glucose was used as the acceptor, no disaccharide
synthesis was detected.
Production of trehalose from sucrose by CES I.
-D-Glucose 1-P is liberated from sucrose by SPase
(Fig. 5). The SPase equilibrium
favors phosphorolysis and yields
-D-glucose 1-P
(12, 29). TSase catalyzes the condensation of
-D-glucose 1-P and D-glucose to trehalose.
When the concentrations of the substrates, sucrose and glucose, were
300 mM each, the optimum temperature was 37.5°C, the optimum pH was
6.5, and the optimum concentration of Pi was 20 mM. Under
these conditions, trehalose was generated from sucrose at a 90 mol%
yield (Fig. 6). The rate of trehalose
synthesis, as determined by the conversion rates in the initial
reaction periods (0 to 4 h), was 18 mmol/h under these conditions
(Fig. 6).
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Production of trehalose from sucrose by CES II. In the CES I system, fructose is generated as a by-product. We expected the fructose to be converted to D-glucose by the action of GIase, which in turn might be incorporated into trehalose by the action of TSase (Fig. 5). We added 20 mM MgSO4 because the GIase used requires Mg2+ and conducted the reaction in an Ar gas atmosphere since weak glucose oxidase-like activity was contained in the GIase. The optimum conditions were 30 to 32.5°C and pH 6.5 to 7.1 (data not shown). The concentration of Pi was not tested extensively, but 20 mM Pi gave an acceptable yield (see below).
The course of trehalose production by CES II under the optimum conditions is shown in Fig. 7. The fructose liberated from the sucrose was rapidly incorporated into trehalose without significant accumulation. Sucrose was converted into trehalose at a 90 mol% yield, the same conversion efficiency as that for CES I. The conversion rate was 4.5 mmol/h (data not shown), which was lower than that in CES I. This slower reaction is probably due to the difference in the concentration of glucose as the substrate in the reaction mixtures; the concentration of glucose in CES I is much higher than that in CES II. In CES I, all of the glucose is immediately available, while the glucose in CES II is gradually supplied by the action of GIase.
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DISCUSSION |
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|
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We have described a novel TSase from a basidiomycete,
G. frondosa, that uses
-D-glucose 1-P as
one of the substrates. The results of screening suggested that
basidiomycetes had relatively higher trehalose phosphorolysis and
synthesis activities than ascomycetes, zygomycetes, and mitosporic
fungi did. An enzyme activity similar to TSase detected in F. velutipes (11) and P. fermentans
(27) was very unstable, and the enzyme was not purified.
Several trehalose phosphorylases reported to date decompose trehalose
to
-glucose 1-P and glucose (4, 15, 17, 34). The TSase in
this study shows no activity toward
-glucose 1-P.
TSase from G. frondosa shows differences in optimum temperature (Fig. 3) and pH (Fig. 4) for the forward and reverse reactions. A similar difference in optimum temperature of the forward and reverse reactions was observed for the trehalose phosphorylase from Euglena (15) and the SPase from Leuconostoc (12), the reason for which is unclear. The great difference in the equilibrium constants for the reactions of the two directions (Fig. 2) may result from this unusual characteristic. TSase from G. frondosa also shows differences in temperature and pH stability for the two directions. It is possible that the activity in one direction can be damaged in some unknown way more than the activity in the other direction.
We found that TSase activity was widespread in the fungi we examined.
Trehalose is believed to be synthesized mainly from trehalose
6-phosphate by the dephosphorylating activity of trehalose 6-P
phosphatase (16). Trehalose 6-P is synthesized from
UDP-glucose and glucose 6-P by the action of trehalose 6-P
synthase (14). Trehalose is also synthesized from
-D-glucose 1-P and glucose by the reversible reaction of
trehalose phosphorylases (1, 4, 15, 19, 33). In
addition, trehalose is synthesized from maltose by the
intramolecular transglucosylating activity of the TSase in
Thermus aquaticus (22) and from
malto-oligosaccharide by the combination of malto-oligosyl
trehalose synthase and malto-oligosyl trehalose trehalohydrolase in an
Arthrobacter sp. (20, 21). It is thus
apparent that trehalose is synthesized by several pathways in a wide
variety of microorganisms. Although the physiological role of this
TSase in G. frondosa is unclear, it is quite possible that the trehalose synthesized from
-D-glucose 1-P and
glucose by the TSase in G. frondosa in the present
study has some physiological role in this strain, which is at present unclear.
For the enzymatic synthesis of trehalose, the TSase from
G. frondosa can be combined with any enzyme that
generates
-D-glucose 1-P. These enzymes include starch
phosphorylase (28),
-1,3-glucan phosphorylase
(2), cellobiose phosphorylase (3), and
laminaribiose phosphorylase (8). Enzymatic processes such as
these often are commercially useful because they are simple, and the
mixture of sugars after the enzyme reaction can often be used directly without further purification. From the commercial point of view, starch
is the most promising substrate. We have conducted preliminary experiments in which TSase and potato starch phosphorylase are combined in a starch-containing reaction mixture. The yield
of trehalose was significant but lower than that in the CES I and CES
II systems (data not shown). Trehalose produced by such a process could
be used in various applications. For example, trehalose is preferred
over sucrose and sorbitol as a food additive for moisturizing
deep-frozen fish, meats, ham, sausage, and noodles. Trehalose improves
the elasticity of these foods and helps prevent discoloration caused by
Maillard's reaction. Greater availability of trehalose at a reduced
price would further increase its use in food processing and preservation.
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FOOTNOTES |
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* Corresponding author. Phone: 81 3 3812 2111, ext. 5123. Fax: 81 3 5802 2931. E-mail: asuhori{at}hongo.ecc.u-tokyo.ac.jp.
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